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Mutual activation between ferrate and calcium sulfite for surface water pre-treatment and ultrafiltration membrane fouling control.
Lian, Jinchuan; Cheng, Xiaoxiang; Zhu, Xuewu; Luo, Xinsheng; Xu, Jingtao; Tan, Fengxun; Wu, Daoji; Liang, Heng.
Afiliação
  • Lian J; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China.
  • Cheng X; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China; Resources and Environment Innovation Institute, Shandong Jianzhu University, Jinan, 250101, PR China. Electronic address: cxx19890823@163.com.
  • Zhu X; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China.
  • Luo X; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China.
  • Xu J; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China.
  • Tan F; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China.
  • Wu D; School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, PR China; Resources and Environment Innovation Institute, Shandong Jianzhu University, Jinan, 250101, PR China.
  • Liang H; State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, Harbin, 150090, PR China.
Sci Total Environ ; 858(Pt 2): 159893, 2023 Feb 01.
Article em En | MEDLINE | ID: mdl-36336042
ABSTRACT
In this work, ferrate (Fe(VI)) and calcium sulfite (CaSO3) were combined to treat surface water for improving ultrafiltration (UF) performance. During the pre-treatment process, the Fe(VI) and CaSO3 activated each other and a variety of active species (Fe(V), Fe(IV), OH, SO4-, 1O2, etc.) were generated. All of the five fluorescent components were effectively eliminated to different extents. With Fe(VI)/CaSO3 = 0.05/0.15 mM, the dissolved organic carbon and UV254 reduced by 44.33 % and 50.56 %, respectively. After UF, these values were further decreased with the removal rate of 50.27 % and 70.79 %. In the UF stage, the terminal J/J0 increased to 0.42 from 0.17, with the reversible and irreversible fouling decreased by 67.08 % and 79.45 % at most. The membrane pore blocking was significantly mitigated, as well as the foulants deposition on membrane surfaces was decreased to some extent. The complete blocking was altered to standard blocking and intermediate blocking, the volume when entering cake filtration was also delayed slightly. The extended Derjaguin-Landau-Verwey-Overbeek theory was employed to judge the interface fouling behavior, and the results indicated that the foulants became more hydrophilic, as well as the adhesion trend between foulants and membrane surface was weakened. Overall, these results provide a theoretical foundation for the practical application of the combined Fe(VI)/CaSO3-UF process in surface water purification.
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Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Ultrafiltração / Purificação da Água Idioma: En Ano de publicação: 2023 Tipo de documento: Article

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Ultrafiltração / Purificação da Água Idioma: En Ano de publicação: 2023 Tipo de documento: Article